US9162946B2ActiveUtilityPatentIndex 45
Process for preparing C3-6 (hydro)fluoroalkenes by dehydrohalogenating C3-6 halo(hydro)fluoroalkanes in the presence of a zinc/chromia catalyst
Est. expiryOct 3, 2026(~0.2 yrs left)· nominal 20-yr term from priority
C07C 17/25C07C 17/358C07C 45/63C07B 2200/09C07C 49/16C07C 17/087C07C 19/10C07C 19/08C07C 17/04C07C 17/18C07C 21/18C07C 17/206C07C 17/23C07C 17/275C09K 5/045C07B 39/00C07C 19/01C09K 2205/126C09K 5/00B01J 23/26C07C 17/21B01J 23/06
45
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Cited by
117
References
21
Claims
Abstract
The invention relates to a process for preparing a C3-6 (hydro)fluoroalkene comprising dehydrohalogenating a C3-6 hydro(halo)fluoroalkane in the presence of a zinc/chromia catalyst, wherein the C 3-6 (hydro)fluoroalkene produced is isomerised in the presence of the zinc/chromia catalyst.
Claims
exact text as granted — not AI-modifiedWe claim:
1. A process for preparing a C 3-6 (hydro)fluoroalkene comprising dehydrohalogenating a C 3-6 hydro(halo)fluoroalkane in the presence of a zinc/chromia catalyst, wherein the C 3-6 (hydro)fluoroalkene produced is isomerised in the presence of the zinc/chromia catalyst.
2. A process according to claim 1 wherein. the C 3-6 (hydro)fluoroalkene exists in E and Z isomers, and the ratio of E and Z isomers is changed in the presence of the zinc/chromia catalyst.
3. A process according to claim 2 wherein the presence of the zinc/chromia catalyst changes the ratio of E and Z isomers from that which is the kinematic determined mixture of isomers from the preparation of the C 3-6 (hydro)fluoroalkene.
4. A process according to claim 2 wherein a desired isomer of the C 3-6 (hydro)fluoroalkene is recovered in a subsequent step.
5. A process according to claim 1 carried out at a temperature of from −70 to 400 °C. and a pressure of from 0 to 30 bara.
6. A process according to claim 1 for preparing a (hydro)fluoropropene comprising dehydrohalogenating a hydro(halo)fluoropropane.
7. A process according to claim 6 wherein the (hydro)fluoropropene produced is selected from tetrafluoropropenes and pentafluoropropenes.
8. A process according claim 7 for preparing 1,2,3,3,3-pentaftuoropropene (CF 3 CF═CHF).
9. A process according to claim 7 for preparing 1,3,3,3-tetrafluoropropene (CF 3 CH═CHF).
10. A process according to claim 7 for preparing 2,3,3,3-tetrafluoropropene (CF 3 CF═CH 2 ) and 1,2,3,3,3-pentafluoropropene (CF 3 CF═CHF).
11. A process according to claim 7 for preparing 2,3,3,3-tetraftuoropropene (CF 3 CF═CH 2 ) and 1,3,3,3-tetrafluoropropene (CF 3 CH ═CHF).
12. A process according to claim 1 wherein the dehydrohalogenating step is carried out in the presence of a feed comprising hydrogen fluoride (HF).
13. A process according to claim 1 wherein the dehydrohalogenating step is carried out in the absence of added hydrogen fluoride.
14. A process according to claim 1 wherein the zinc chromia catalyst comprises 0.01 % to 25% by weight zinc.
15. A process according to claim 1 wherein the zinc chromia catalyst is amorphous or from 0,1 to 50% by weight of the catalyst is in the form of one or more crystalline compounds of chromium and/ or more crystalline compounds of zinc.
16. A process according to claim 5 wherein the process is carried out in the vapour phase at a temperature of from 200 to 360° C.
17. A process according to claim 5 wherein the process is carried out at super-atmospheric pressure.
18. A process according to claim 1 wherein the process is carried out with a diluent gas.
19. A process according to claim 18 wherein the diluent gas comprises nitrogen.
20. A process according to claim 18 wherein the diluent gas comprises the resultant C 3-6 (hydro) fluoroalkene or an isomer rich blend of the C 3-6 hydro)fluoroalkene.
21. A process according to claim 1 wherein the process is carried out in the presence of HF and at atmospheric or sub-atmospheric pressure and wherein the ratio of HF to hydro(halo)fluoroalkane is greater than 1.5:1.Cited by (0)
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